Non-Newtonian turbulence: viscoelastic fluids and binary mixtures.
Non-Newtonian turbulence: viscoelastic fluids and binary mixtures.
Non-Newtonian turbulence: viscoelastic fluids and binary mixtures.
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20 1. <strong>Newtonian</strong> <strong>turbulence</strong><br />
Figure 1.3: Probability distributions, normalized with their st<strong>and</strong>ard deviations<br />
σr =< δu 2 r >1/2 , of transverse velocity increments in a turbulent air jet at Rλ =<br />
695 for different separations: r ∼ η (dotted line); r ∼ ℓ0 shifted of three decades<br />
(long dashed line); intermediate scales (solid line) [13].<br />
A phenomenological model of intermittency is the multifractal one, introduced<br />
by Parisi <strong>and</strong> Frisch [14]. In the multifractal approach [14, 15], instead of global<br />
scale invariance, local scale invariance is assumed; more specifically, hypothesis<br />
H2 is modified into:<br />
HMF in the limit Re → ∞, the turbulent flow possesses a range of scaling<br />
exponents I = [hmin, hmax]. For all h ∈ I, there is a set Sh ⊂ R3 of<br />
dimension D(h), such that for x ∈ I <strong>and</strong> ℓ → 0:<br />
� �h δuℓ(x) ℓ<br />
∼<br />
(1.60)<br />
u0<br />
where, of course, u0 is the large scale velocity.<br />
The structure function of order p is then expressed as a superposition, weighted<br />
with a measure dµ(h), of different contributions originated by different scaling<br />
exponents:<br />
Sp(ℓ)<br />
u p<br />
0<br />
�<br />
∼<br />
I<br />
ℓ0<br />
� �ph+3−D(h) ℓ<br />
dµ(h)<br />
ℓ0<br />
(1.61)<br />
where the factor (ℓ/ℓ0) 3−D(h) is the probability of being within a distance ℓ of the<br />
set Sh. The exponent ζp can be obtained in the limit ℓ → 0 by a saddle-point<br />
20